Conversion of Aluminum Phosphate to Sodium Phosphate

Total Page:16

File Type:pdf, Size:1020Kb

Conversion of Aluminum Phosphate to Sodium Phosphate Journal of Materials Science and Engineering A 6 (11-12) (2016) 321-325 doi: 10.17265/2161-6213/2016.11-12.005 D DAVID PUBLISHING Conversion of Aluminum Phosphate to Sodium Phosphate Masaaki Takahashi1*, Yukimasa Takemoto1, Maki Ooyagi1, Ken Oonishi2 and Eiji Yuuki2 1. Yokkaichi University, Research Laboratory on Environmental Technology, Kayo-cho 1200, Yokkaichi, Mie, 512-8512, Japan 2. Mie Chuo Kaihatsu Co., Ltd, Hachiya4713, Yono, Iga, Mie, 518-1152, Japan Abstract: The phosphorus recovered from sewage sludge by acidic treatment is mainly composed of aluminum phosphate. To make a wide utilization of recovered phosphorus, removal of the aluminum component is considered a very important matter. In order to find a method to convert aluminum phosphate to sodium phosphate, a basic investigation was carried out. A reagent of aluminum phosphate was dissolved by aqueous solution of sodium hydroxide, and mixed with sodium silicate to make a alunino-silicate gel. Sodium phosphate was recovered from residue water in the gel. Key words: Aluminum phosphate, sodium phosphate, gelation, sodium silicate. 1. Introduction where M is alkali metal, m, n, x, y and z are indefinite numbers. Sewage sludge contains significant amounts of In order to confirm this method, we investigated the phosphorus, and in order to recover the phosphorus, reaction using a reagent of sodium hydroxide, some studies have been carried out [1-6]. The aluminum phosphate and sodium silicate. phosphorus which is recovered by acidic treatment contains a lot of aluminum [7]. To make a wide 2. Method utilization of recovered phosphorus, the removal of 2.1 Preparation the aluminum component is considered a very important matter, and some methods were investigated In this experiment, sodium hydroxide: Kanto [8]. chemical Co., INC (assay minimum 97%), aluminum The aluminum component in the recovered phosphate: Kanto chemical Co., INC (assay minimum phosphorus is considered to exist mainly as a form of 95 % as AlPO4), sodium silicate: Kanto chemical Co., aluminum phosphate. Aluminum ion reacts with alkali INC (assay minimum SiO2: 37%, Na2O: 18%) was metal silicate to form a silicate gel, which is widely used. known as zeolite synthesis. Aluminum phosphate is Aqueous solutions of these reagents were prepared dissolved by the addition of aqueous solution of alkali as mentioned below: metal hydroxide, and is also expected to react with Aq. aluminum phosphate solution: 50 g of alkali metal silicate to make an alkali metal silicate aluminum phosphate was resolved by addition of 50 g gel. Using this reaction, alkali metal phosphate is of sodium hydroxide in 1,000 mL of water. considered to be recovered as reaction (1) [9]. Aq. sodium silicate solution: 100 g of sodium silicate was in 100 mL of water (total volume 155 MSiO23 mAlPO 4 nMOH (1) mL). MOxAlO2232234 ySiO zHO MPO 2.2 Experimental Procedure *Corresponding author: Masaaki Takahashi, researcher, research field: environmental technology. The experiment was carried out as shown in Fig. 1. 322 Conversion of Aluminum Phosphate to Sodium Phosphate Aq. aluminum phosphate solution Aq. sodium silicate solution Extract Solution Gelation Frieze, de-freezing Separation Evaporation Residue Gel Phosphorus Fig. 1 Experimental procedure. Aq. sodium silicate solution was added to the aq. of pH 11.5. The formed gel was cooled in an ice box, solution of aluminum phosphate at room temperature and dehydration was carried out as mentioned before. and the mixture formed a transparent gel. In order to The dehydrated gel was dried and the phosphorus estimate the amount of the gel, dehydration is needed. containing extract was evaporated for analysis, and gel To make rapid dehydration, a freezing and de-freezing (17 g) and phosphorus, (23 g) were recovered. method applied to the dehydration of sludge [10], was 3. Result and Discussion carried out. The formed gel was cooled in an ice box (under -10 ºC) for one day, later, the frozen gel was 3.1 Addition Rate retained at a room temperature (about 25 ºC) to make The relation of the amount of the formed gel and de-freezing. The dehydration was brought about the addition rate of the sodium silicate is shown in through de-freezing, and the dehydrated gel was Fig. 2. The amount of the formed gel, increased by separated by filtration, and the residue was dried at addition of sodium silicate, and when the addition rate 105 ºC for analysis. The phosphorus component was reached 10g, amount of the gel tends to plateau. This recovered from the extract through evaporation. addition rate is considered to correspond to a 2.3 Addition Rate molecular ratio Al2O3 : SiO2 = 0.35 : 1. In order to find a proper addition rate, 5 mL to 20 3.2 Properties of Recovered Materials mL of aq. sodium silicate solution was added to 100 The recovered gel is a white powder, particle size: mL of aq. aluminum phosphate solution at room under 0.05 mm as shown in Fig. 3, bulk density: temperature (about 25 ºC), and the mixture formed a 0.2~0.3 g/cm3. The chemical component of the gel in a few minutes. The formed gel was cooled in an recovered gel and phosphorus was analyzed by X-ray ice box for 24 hours, and the frozen gel was retained in a room for de-freezing. Dehydration took place Gel (g) through de-freezing, and the dehydrated gel was 8 7 separated using filter paper (ADVANTEC, No2, Toyo 6 Roshi Co LTD), and residue (gel) was dried at 105 ºC 5 4 for analysis. 3 2 2.4 Recovery of Phosphorus 1 0 A 200 mL of aq. aluminum phosphate solution was 0 5 10 15 mixed with a 30 mL of aq. sodium silicate solution at Sodium silicate (g) room temperature, and a gel was formed in a condition Fig. 2 Relation of sodium silicate and formed gel. Conversion of Aluminum Phosphate to Sodium Phosphate 323 chemical composition of the raw material was calculated by mass balance of the reagent used in this experiment. The recovered gel was composed of Na2O、SiO2、Al2O3, and it was considered to be a compound of alumino- silicate. The elemental ratio of the gel was calculated from the analyzed data and the approximate molecular ratio was considered as (2). Na2O·xAl2O3·ySiO2; x/y = 1/ 3 (2) The ratio of x : y corresponds to the chemical composition of a zeolite [11]. However, XRD of the gel shows the pattern of an amorphous compound Fig. 3 Photo of the gel. (Fig. 5), and further investigation is needed to identify some properties and physical structure. 100% The amount of P2O5 component in the gel is small, 80% others 60% and almost of all the phosphorus was separated from P2O5 40% the gel as an extract. The recovered phosphorus was Al2O3 20% Na2O composed of P2O5 and Na2O, and is considered to be a 0% form of Na2HPO4·7H2O by the XRD analysis (Fig. 6) Raw Gel Crystal SiO2 material and recovered condition (pH11-pH12) [12]. A small amount of SiO2 component was found in Fig. 4 Chemical composition of recovered materials. the recovered phosphorus, which is considered analyzer, (XRF, Rigaku Corporation SPECTRO non-reacted sodium silicate which remained in the XEPOS) and the result is shown in Fig. 4. The recovered phosphorus. Counts Fig. 5 XRD spectrum of the gel. 324 Conversion of Aluminum Phosphate to Sodium Phosphate Counts Na2HPO4 Na2HPO4 7H2O Na2SiO3 9H2O Na2SiO3 5H2O Fig. 6 XRD spectrum of the recovered crystal. 4. Conclusions Ohtake, H. and Miura, K. et al. 2013. “Novel Technique for Phosphorus Recovery from Aqueous Solutions Using In order to find a wide utilization of aluminum Amorphous Calcium Silicate Hydrates (A-CSHs).” Water phosphate which is recovered from sewage sludge, a Research 47 (7): 2251-9. [3] Nakahara, K. 2001. “Vitrification Process for Recovery conversion method of aluminum phosphate to sodium of Phosphorus/Phosphoric Acid from Sewage Sludge phosphate was investigated using a reagent of Ash.” Industrial Water 514: 2-10. aluminum phosphate. Aluminum phosphate which [4] Sonoda, K., Tokukura, K., Mori, T., Komazawa, I. and was dissolved by sodium hydroxide reacted with Wada, T. 1996. “Phosphoric Acid Recovering from Incinerated Ashes of Sewage Treatment Sludge.” In sodium silicate, and formed a silicate gel. Aluminum Proceedings of the 7th Annual Conference of the Japan phosphate was converted to sodium phosphate Society of Waste Management Expert, 267-9. through the formation of alumino-silicate gel. The [5] Ingham, J., Ryan, J., Keyakida, E. and Ri, J. 1996. “Phosphorus and Metal Recovery from Sewage result indicates a possibility to make a recovery Treatment Sludge.” In Proceedings of the 7th Annual method of sodium phosphate from sewage sludge. Conference of the Japan Society of Waste Management However, further study is needed to investigate the Expert, 280-2. conversion of sodium phosphate from aluminum [6] Yoshida, K., Takahashi, Y. and Hatano, M. 2001. “The Experiment on the Recovering pf Sodium Phosphate from phosphate which is recovered from sewage sludge. Incinerated Ash of Sewage Sludge.” In Proceedings of Reference the 12th Annual Conference of the Japan Society of Waste Management Expert, 280-2. [1] Shima, H. and Takahashi, M. 1997. Gekkan [Mizu] [7] Takahashi, M., Takemoto, Y. and Oonishi, K. 2013. Publishing, Gekkan Water (In Japanese). 39-7 (552): “Recovery of Aluminum Phosphate Using Magnesium 36-40. hydroxide from Incinerated Ash of Sewage Sludge.” [2] Okano, K., Umemoto, M., Kagami, J., Honda, K., Journal of Material Science and Engineering A 3 (10): Conversion of Aluminum Phosphate to Sodium Phosphate 325 710-3. [10] Tezuka, M., Asano, T., Toba, A., Cobayasi, Y., Isioka, M. [8] Sato, K., Takahashi, M., Onari, Y., Kato, S. and Enjyoji, and Taziri, K. et al. 1995. “Treatment of Waste, -Solution H.
Recommended publications
  • An Improved Process for the Production of Cumene
    Europaisches Patentamt European Patent Office © Publication number: 0 537 389 A1 Office europeen des brevets EUROPEAN PATENT APPLICATION © Application number: 91309531.1 int. Ci.5; C07C 2/66, C07C 2/86, C07C 6/12, C07C 15/085 (§) Date of filing: 16.10.91 ® Date of publication of application: @ Applicant: Council of Scientific and Industrial 21.04.93 Bulletin 93/16 Research Rafi Marg @ Designated Contracting States: New Delhi 110 001 (IN) BE DE FR GB IT NL @ Inventor: Pradhan, Ajit Ramchandra National Chemical Laboratory Pune-411008, Maharashtra(IN) Inventor: Rao, Bollapragad Seshagiri National Chemical Laboratory Pune-411008, Maharashtra(IN) 0 Representative: Collier, Jeremy Austin Grey et al J.A.Kemp & Co., 14 South Square, Gray's Inn London WC1R 5LX (GB) 0 An improved process for the production of cumene. © An improved process is disclosed for the preparation of cumene. Cumene is prepared by reacting benzene with a propylating agent in the presence of a catalyst containing metal loaded Zeolite EU-1 in a reactor in the range of a temperature of 150 to 250 °C and a pressure of 1 to 35 atmospheres, the propyl and diisopropylben- zene so formed are separated from the reactor effluent by conventional methods. The diisopropylbenzene is recycled back to the reactor. Simultaneous alkylation and transalkylation reactions occur in a single catalyst bed containing Zeolite EU-1 with a feed containing benzene, propylene and diisopropylbenzene. Cumenes are important chemical precursors in the production of detergents and polymers among others. Oi CO CO IV CO m Rank Xerox (UK) Business Services (3. 10/3.5x/3.0.
    [Show full text]
  • 5. POTENTIAL for HUMAN EXPOSURE 5.1 OVERVIEW White
    WHITE PHOSPHORUS 157 5. POTENTIAL FOR HUMAN EXPOSURE 5.1 OVERVIEW White phosphorus can enter the environment from its production, use, accidental spills during loading and unloading for shipment, and accidental spills during transport. Hazardous wastes sites containing white phosphorus can also be a source of phosphorus in the environment. White phosphorus has been found in at least 77 of the 1,430 current or former EPA National Priorities List (NPL) hazardous waste sites (HazDat 1996). However, the number of sites evaluated for white phosphorus is not known. The frequency of these sites within the United States can be seen in Figure 5-l. The persistence of elemental phosphorus in the air is very short due to oxidation to phosphorus oxides and ultimately to phosphorus acids. However, the particulate phosphorus aerosol may be coated with a protective oxide layer that may prevent further oxidation and extend the lifetime of particulate phosphorus in air. Both wet and dry deposition remove unreacted elemental phosphorus and the degradation products from the air. Similarly, elemental phosphorus oxidizes and hydrolyzes in water and in soil. A small amount of elemental phosphorus is lost from soil and water by volatilization. Phosphorus is used as a fumigant in the storage of grain. Because of ease of application, pellets of aluminum or magnesium phosphide are commonly used (Garry et al. 1993). Phosphine, a highly toxic gas, is generated from phosphide. The rate of formation of phosphine (permissible exposure limit [PEL], 0.4 mg/m3) is dependent on the ambient temperature and humidity. Its release is rapid, and it is extremely fatal to the unprotected person (Garry et al.
    [Show full text]
  • Phosphoric Acid 706-798-4346 Section 1.0 Product and Company Information
    MATERIAL SAFETY DATA SHEET PRAYON INC. P.O. Box 1473 1610 Marvin Griffin Road Augusta, GA 30903-1473 PHOSPHORIC ACID 706-798-4346 SECTION 1.0 PRODUCT AND COMPANY INFORMATION PRODUCT NAME: PHOSPHORIC ACID (36-85%) MSDS Number: P007664382 Chemical Name: Phosphoric acid MSDS Origination Date: 10/01/2000 Synonyms: Phos acid, orthophosphoric acid MSDS Revision Date: 01/05/2006 IN THE EVENT OF A CHEMICAL EMERGENCY, SPILL, LEAK, FIRE, EXPOSURE, OR ACCIDENT Call CHEMTREC: 1-800-424-9300. Toll free in the continental U.S., Hawaii, Puerto Rico, Canada, Alaska, or U.S. Virgin Islands. For calls originating elsewhere dial 703-527-3887 (collect calls accepted). For additional non-emergency information call: 706-798-4346 SECTION 2.0 COMPOSITION / INGREDIENTS INFORMATION Component CAS No. % By Weight OSHA PEL* ACGIH TLV* Phosphoric acid 7664-38-2 36-85 1 mg/m3 1 mg/ m3 Water 7732-18-5 15-64 N/A N/A *Based on 8-hour time weighted averages SECTION 3.0 HAZARD IDENTIFICATION WARNING STATEMENTS: DANGER: CAUSES EYE AND SKIN BURNS MAY BE HARMFUL IF SWALLOWED CORROSIVE TO MILD STEEL EMERGENCY OVERVIEW: APPEARANCE AND ODOR: Slightly viscous, clear liquid with no odor POTENTIAL HEALTH EFFECTS: Likely Routes of Entry: Skin & Eye contact EYE CONTACT: This product can cause serious eye burns. Damage may be permanent. SKIN CONTACT: Corrosive to the skin. Causes burns. Burning may be delayed. INHALATION: Breathing of vapor or mist may be irritating to the respiratory tract. Serious cases of inhalation may cause respiratory problems and late pulmonary edema. INGESTION: May be harmful if swallowed.
    [Show full text]
  • United States Patent 0 "Ice Patented Mar
    3,504,046 United States Patent 0 "Ice Patented Mar. 31, 1970 1 2 higher temperature would make such a difference in the 3 504,046 ALKYLATION OF NAPHTHALENE WITH PRO isomer product ratio. PYLENE IN THE PRESENCE OF PHOSPHORIC In accordance with the present invention the solid ACID CATALYST phosphoric acid catalyst and the naphthalene are charged Edward Jonathan Scharf, Somerville, and Herbert Ru into a suitable reaction vessel, such as an autoclave. The ‘dolph Kemme, Piscataway, N.J., assignors to American system is purged with nitrogen and then with propylene. Cyanamid Company, Stamford, Conn., a corporation of The mixture is then heated to the desired temperature, Maine agitation started and the reaction allowed to proceed un No Drawing. Filed Apr. 26, 1968, Ser. No. 724,626 der autogenous pressure. Upon completion of the reac Int. Cl. C07c 3/54 10 tion, the reactor is cooled, the product mixture with US. Cl. 260-671 2 Claims drawn and the catalyst separated. Any of the solid phosphoric acid catalysts disclosed ABSTRACT OF THE DISCLOSURE in US. Patent Nos. 2,575,457, 2,584,102, 3,183,233 and 3201,486 may be used in the invention. In general, The alkylation of naphthalene with propylene in the 15 they are comprised of phosphoric acid on an inert presence of solid phosphoric acid catalysts is conducted support, such as kieselguhr. They are used in the alkyla at temperatures above about 300° 0., whereby the ratio tion reaction in an amount, based on the total weight of beta- to alpha-isopropyl naphthalene in the product of naphthalene and proylene used, of at least about 1% is substantially increased.
    [Show full text]
  • Preparation of Diammonium Hydrogenphosphate Student Worksheet
    Preparation of diammonium hydrogenphosphate Student worksheet Diammonium hydrogenphosphate (DAP) is a simple salt, but a complex fertiliser, as it is a source of two nutrients – nitrogen and phosphorous. It can be made by partially neutralising dilute phosphoric acid with dilute ammonia solution. Ammonia is titrated with phosphoric acid using methyl orange indicator to find the volume of acid that reacts with 10 cm3 of ammonia to form ammonium dihydrogenphosphate: H3PO4(aq) + NH3(aq) NH4H2PO4(aq) Then you add this volume of acid to 20 cm3 of ammonia to form diammonium hydrogen phosphate. H3PO4(aq) + 2NH3(aq) (NH4)2HPO4(aq) Equipment and materials • Evaporating basin • Filter funnel, filter paper and conical flask (to stand funnel on) • Tripod and gauze • Glass rod. • Bunsen burner • 1 mol dm−3 phosphoric acid • 10 cm3 pipette • 1 mol dm−3 ammonia solution • Burette and stand • Methyl orange indicator solution • 100 cm3 conical flask Method Care: Wear eye protection. 1 mol dm−3 ammonia solution and 1 mol dm−3 phosphoric acid are irritants to the eyes, lungs and the respiratory system. Work in a well-ventilated lab. 1. Use a pipette to transfer 10 cm3 of 1 mol dm−3 ammonia solution to a conical flask. Add a few drops of methyl orange indicator to the conical flask, and stand it on a white background. 2. Note the initial burette reading before adding 1 mol dm–3 phosphoric acid to the flask from a burette until the indicator changes colour. Make a note of the volume of acid added. 3. Use a pipette to transfer 20 cm3 of 1 mol dm−3 ammonia solution to an evaporating basin.
    [Show full text]
  • Influence of Ph-Control in Phosphoric Acid Treatment of Zinc Oxide
    Cerâmica 63 (2017) 197-202 http://dx.doi.org/10.1590/0366-69132017633662149 197 Influence of pH-control in phosphoric acid treatment of zinc oxide (Influência do controle do pH no tratamento de óxido de zinco com ácido fosfórico) H. Onoda1, M. Chemel2 1Department of Informatics and Environmental Sciences, Kyoto Prefectural University, 1-5, Shimogamo Nakaragi-cyo, Sakyo-ku, Kyoto 606-8522, Japan 2Ecol de Biologie Industrielle, 32 Boulevard du Port, 95094 CERGY Cedex, France [email protected] Abstract Zinc oxide is often used as a white pigment for cosmetics; however, it shows photocatalytic activity that causes decomposition of sebum on the skin when exposed to the ultraviolet radiation in sunlight. In this work, zinc oxide was reacted with phosphoric acid at various pH values to synthesize a novel white pigment for cosmetics. The chemical composition, powder properties, photocatalytic activities, colors, and smoothness of these pigments were studied. The obtained materials exhibited X-ray diffraction peaks relating to zinc oxide and phosphate after phosphoric acid treatment. The ratio of zinc phosphate to zinc oxide was estimated from inductively coupled plasma - atomic emission spectroscopy results. Samples treated at pH 4-7 yielded small particles with sub-micrometer sizes. The photocatalytic activity of zinc oxide became lower after phosphoric acid treatment. Samples treated at pH 4-7 showed the same reflectance as zinc oxide in both the ultraviolet and visible ranges. Adjustment of the pH was found to be important in the phosphoric acid treatment of zinc oxide. Keywords: zinc oxide, phosphoric acid treatment, photocatalytic activity, particle size. Resumo O óxido de zinco é comumente usado como um pigmento branco para cosméticos; entretanto, apresenta atividade fotocatalítica que provoca a decomposição do sebo na pele quando exposto à radiação ultravioleta na luz solar.
    [Show full text]
  • Aluminum Phosphates
    Dr. Ralf Giskow, The Variety of Phosphates Jörg Lind, Erwin Schmidt Chemische Fabrik Budenheim KG, for Refractory and Technical D-55257 Buden- heim www.budenheim- Applications by the Example cfb.com of Aluminium Phosphates In 1669 the chemical element phos- Phase-I-content influences, for phorus was discovered by H. Brandt, example, the dissolution property of an alchemist. In 1694 Boyle made STPP in water. The choice of the the first phosphoric acid by dissolv- right phosphate can already be the ing phosphorus pentoxide (P2O5) in crucial point even with such a “sim- water. This was the start of the phos- ple“ phosphate like sodium tripoly- phorus chemistry. Since this time phosphate. phosphoric acid and its salts have a The next step into the direction firm place in chemistry and technical of complexity is a phosphate called applications. Phosphates are part of sodium hexametaphosphate (SHMP) our life and are used in a variety of in colloquial language. In fact, the ways also in industrial fields like chemical name is a mistake. The refractories, glass, ceramics, con- name sodium hexametaphosphate struction industry and for a lot of would stand for a sodium phosphate other technical purposes. with a ring structure (“meta”). But SHMP has a chaintype structure as can be proved. These melted glassy polyphosphates (SHMP) with pH-val- Fig. 1 Phosphates in Refractory phosphates are polyphosphates with ues between three and nine, most of FABUTIT 734, a modified STPP and Technical Industries different chain lengths. The average the products also in an instantised against a standard The most common and well known chain length and thus the properties quality (Fig.
    [Show full text]
  • Low Temperature Phosphoric Acid Treatment of Zinc Oxide for Nobel White Pigments
    Ceramics-Silikáty 63 (3), 291-296 (2019) www.ceramics-silikaty.cz doi: 10.13168/cs.2019.0023 LOW TEMPERATURE PHOSPHORIC ACID TREATMENT OF ZINC OXIDE FOR NOBEL WHITE PIGMENTS #HIROAKI ONODA, DAIKI HIGASHIDE Department of Informatics and Environmental Sciences, Kyoto Prefectural University, 1-5, Shimogamo Nakaragi-cyo, Sakyo-ku, Kyoto 606-8522, Japan #E-mail: [email protected] Submitted March 15, 2019; accepted accepted April 27, 2019 Keywords: Zinc oxide, Photocatalytic activity, Powder processing Zinc oxide that has the photocatalytic activity is used as white pigment for cosmetics. A certain degree of sebum on the skin is decomposed by the ultraviolet radiation in sunlight. In this work, zinc oxide was shaken with phosphoric acid to synthesize a white pigment for cosmetics. Zinc oxide was set with 0.1 mol∙l-1 of phosphoric acid at P/Zn = 1/1 and 1/2, and then shaking in water at 30, 40, 50 °C for 1, 3, 6 hours. The chemical composition, powder properties, photocatalytic activity, color phase, and smoothness of the obtained powder were studied. The P/Zn ratio in preparation had influence on the reaction between phosphoric acid and zinc oxide. The photocatalytic activity of zinc oxide was inhibited by phosphoric acid treatment. The treated samples at 50 °C had enough high reflectance at the visible light region. INTRODUCTION difficult to determine because the pore sizes of the skin are affected by such factors as age, gender, and climate As a white pigment, zinc oxide is used for cosmetic [9]. Furthermore, overly large particles are inappropriate applications [1].
    [Show full text]
  • 140. Sulphuric, Hydrochloric, Nitric and Phosphoric Acids
    nr 2009;43(7) The Nordic Expert Group for Criteria Documentation of Health Risks from Chemicals 140. Sulphuric, hydrochloric, nitric and phosphoric acids Marianne van der Hagen Jill Järnberg arbete och hälsa | vetenskaplig skriftserie isbn 978-91-85971-14-5 issn 0346-7821 Arbete och Hälsa Arbete och Hälsa (Work and Health) is a scientific report series published by Occupational and Enviromental Medicine at Sahlgrenska Academy, University of Gothenburg. The series publishes scientific original work, review articles, criteria documents and dissertations. All articles are peer-reviewed. Arbete och Hälsa has a broad target group and welcomes articles in different areas. Instructions and templates for manuscript editing are available at http://www.amm.se/aoh Summaries in Swedish and English as well as the complete original texts from 1997 are also available online. Arbete och Hälsa Editorial Board: Editor-in-chief: Kjell Torén Tor Aasen, Bergen Kristina Alexanderson, Stockholm Co-editors: Maria Albin, Ewa Wigaeus Berit Bakke, Oslo Tornqvist, Marianne Törner, Wijnand Lars Barregård, Göteborg Eduard, Lotta Dellve och Roger Persson Jens Peter Bonde, Köpenhamn Managing editor: Cina Holmer Jörgen Eklund, Linköping Mats Eklöf, Göteborg © University of Gothenburg & authors 2009 Mats Hagberg, Göteborg Kari Heldal, Oslo Arbete och Hälsa, University of Gothenburg Kristina Jakobsson, Lund SE 405 30 Gothenburg, Sweden Malin Josephson, Uppsala Bengt Järvholm, Umeå ISBN 978-91-85971-14-5 Anette Kærgaard, Herning ISSN 0346–7821 Ann Kryger, Köpenhamn http://www.amm.se/aoh
    [Show full text]
  • Optimizing Dilute Phosphoric Acid Pretreatment of Wheat Straw in The
    Optimizing dilute phosphoric acid pretreatment of wheat straw in the laboratory and in a demonstration plant for ethanol and edible fungal biomass production using Neurospora intermedia Short title: Ethanol and edible filamentous fungal biomass from pretreated wheat straw Ramkumar B. Nair*, Magnus Lundin, Patrik R. Lennartsson, Mohammad J. Taherzadeh Swedish Centre for Resource Recovery, University of Borås, SE 50190 Borås, Sweden *Corresponding author Tel: +46 33 4355903 Fax: +46 33 4354003 E-mail: [email protected] Accepted Article This article has been accepted for publication and undergone full peer review but has not been through the copyediting, typesetting, pagination and proofreading process, which may lead to differences between this version and the Version of Record. Please cite this article as doi: 10.1002/jctb.5119 This article is protected by copyright. All rights reserved. Abstract BACKGROUND: We report a method that uses dilute phosphoric acid for wheat straw pretreatment and subsequent ethanol and fungal biomass production with the edible fungus Neurospora intermedia. Dilute phosphoric acid pretreatment of wheat straw was optimized at a laboratory scale, and the results were validated in a biorefinery demonstration plant for the first time. The various conditions for the dilute acid pretreatment include such factors as phosphoric acid concentrations (0.5–3.0% w/v), temperature (150–210°C), and reaction time (5–20 min). RESULTS: The optimal pretreatment conditions were determined as an acid concentration of 1.75% (w/v) at a temperature of 190°C for 15 min, based on the maximum enzymatic digestibility with the minimum inhibitor release. The efficiency of enzymatic polysaccharide hydrolysis was 36% for untreated straw and 86% for straw pretreated with dilute phosphoric acid.
    [Show full text]
  • Phosphorous Acid Labeling Aid
    PHOSPHOROUS ACID LABELING AID 1. Does your product contain only phosphorous acid (H3PO3)/Phosphite as a source of phosphorus? Adhere to the format presented in § 2309(a). i. X% Total phosphoric acid must be guaranteed. Total Phosphoric Acid (P2O5) % ii. State phosphate as zero in the grade (N-0-K) or include an asterisk (N-P*-K) to clarify the phosphorus stated in the grade is not in the available phosphate form. iii. Include required statements according to § 2309(a)(1)(2)(3). If an asterisk is used in the grade, an asterisk must be used before each required statement (e.g. “*(1) Phosphorous acid products…”, “*(2) Upon foliar…”). 2. Does your product contain BOTH phosphorous acid (H3PO3)/phosphite AND phosphoric acid (H3PO4)/phosphate? Adhere to format presented in § 2309(b): i. X% Available phosphoric acid must be guaranteed. Available Phosphoric Acid (P2O5) % ii. X% Total phosphoric acid must be guaranteed. % Total Phosphoric Acid (P2O5) iii. X% Insoluble phosphoric acid must be guaranteed (if present). % Insoluble Phosphoric Acid (P2O5) iv. Report percentage of available phosphate in the grade. v. Include heavy metals statement on the label and submit heavy metals analysis. vi. Include required statements according to § 2309(a)(1)(2)(3). Required statements [§ 2309(a)(1)(2)(3)]: (1) Phosphorous acid products are for use as a supplemental fertilizer treatment. (2) Upon foliar application, the phosphite ions are taken up directly by the plant foliage and may undergo a degree of conversion to phosphate ions, or will be used directly by plants, as phosphite ions. (3) As a soil application to annual crops, a lesser response from the initial crop, with a corresponding superior response from succeeding crops, may be observed.
    [Show full text]
  • United States Patent Office Patiented Nov
    3,112,180 United States Patent Office Patiented Nov. 26, 1963 2 borohydride and diborane gas is evolved. The preferred 3,12,130 method of conducting the reaction is to dissolve the weak METHOD FOR THE PREPARATION OF D30RANE inorganic acid, salt or ester in the sulfuric or chloro Rosert D. Schaatz, East Whittier, Calif., assig or to sulfonic acid, with heating if necessary to effect solution. Aerojet-General Corporation, Azusa, Calif., a corpora The reaction is usually conducted in a reactor equipped tion of Ohio with a gas outlet leading to a low temperature trap. No Drawing. Filled Mar. 10, 1955, Ser. No. 493,570 The acid solution is placed in the reactor and finely 17 Caians. (C. 23-224) divided borohydride added with agitation. During the This invention relates to a new and improved method course of the reaction, a gentle evolution of hydrogen of preparing diborane. IO) and diborane gases takes place. These gases are vented Diborane is an excellent high energy fuel. Unfor through the gas outlet and collected in the low tempera tunately, however, its use has been severely limited due ture trap. If desired, the reaction can also be conducted to a lack of a convenient and inexpensive method for in vacuum or a nitrogen atmosphere as well as in air. preparing it in high yield. To more clearly illustrate this invention, the following Heretofore, diborane has been prepared by reacting examples are presented. It is to be understood, however, alkali metal borohydrides with hydrogen chloride gas that these examples are presented merely as a means of at room temperature or with liquid hydrogen chloride illustration and are not intended to limit the scope of at a temperature of -78° C.
    [Show full text]